CN201964680U - Carbon dioxide self-driving refrigeration system - Google Patents
Carbon dioxide self-driving refrigeration system Download PDFInfo
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- CN201964680U CN201964680U CN2011200513076U CN201120051307U CN201964680U CN 201964680 U CN201964680 U CN 201964680U CN 2011200513076 U CN2011200513076 U CN 2011200513076U CN 201120051307 U CN201120051307 U CN 201120051307U CN 201964680 U CN201964680 U CN 201964680U
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Abstract
The utility model relates to a carbon dioxide self-driving refrigeration system which consists of a carbon dioxide cylinder, a needle valve, a first cooling heat exchanger, a second cooling heat exchanger, a first capillary tube, a gas-liquid separator, an evaporator, a fan, a second capillary tube, a heat exchanger and a valve that are connected one another in sequence by pipes, wherein an output end of the carbon dioxide cylinder is connected with a first input end of the first cooling heat exchanger, a first output end of the cooling heat exchanger is connected with a first input end of the second cooling heat exchanger, and a first output end of the second cooling heat exchanger is connected with an input end of the first capillary tube. Known from the technical scheme, the carbon dioxide self-driving refrigeration system mainly adopts the characteristics of high refrigeration quantity of unit-volume carbon dioxide and high evaporation pressure of the carbon dioxide, the separated carbon dioxide is pressed into the evaporator for evaporation and refrigeration by utilizing the inner pressure of the carbon dioxide cylinder, refrigeration in corresponding time can be provided according to gas accumulation capacity of the carbon dioxide cylinder, and refrigeration under no any external power driving condition is realized.
Description
Technical field
The utility model relates to air-conditioning refrigeration system, relates to the self-driven refrigeration system of a kind of carbon dioxide specifically.
Background technology
At present, the driving that refrigeration system all needs extrinsic motive usually can realize refrigeration, but under power electricity or the whole situations of scattering and disappearing of standby electricity, some visual plant, still have refrigeration demand as equipment such as high-end electronic devices, instrument, hospital, weaponrys, guarantee its within a certain period of time can safe operation with close, at this moment under the environment that does not have extrinsic motive to drive, refrigeration just can't realize.
Summary of the invention
The purpose of this utility model provides the self-driven refrigeration system of a kind of carbon dioxide, can guarantee local room temperature control within a certain period of time under the environment that drives without any external force.
For achieving the above object, the utility model has adopted following technical scheme: be connected in sequence by pipeline by dioxide bottle, needle-valve, first cooling heat exchanger, second cooling heat exchanger, first capillary, gas-liquid separator, evaporimeter, blower fan, second capillary, heat exchanger, valve, the output of dioxide bottle links to each other with the first input end of first cooling heat exchanger, first output of first cooling heat exchanger links to each other with the first input end of second cooling heat exchanger, and first output of second cooling heat exchanger links to each other with first input capillaceous.
First cooling heat exchanger of the present utility model also is provided with second input and second output, and described second cooling heat exchanger also is provided with second input and second output.
The gas output end of gas-liquid separator of the present utility model links to each other with second input of second cooling heat exchanger, and second output of second cooling heat exchanger links to each other with the input of blower fan.
The output of evaporimeter of the present utility model links to each other with second input of first cooling heat exchanger, and second output of first cooling heat exchanger links to each other with the input of blower fan.
Be provided with liquid-sighting glass, Pressure gauge and thermometer successively between the liquid output of gas-liquid separator of the present utility model and the evaporimeter.
Blower fan of the present utility model is pneumatic blower fan.
Valve of the present utility model comprises check valve and ball valve, and the output of heat exchanger links to each other with the input of check valve, and the output of check valve links to each other with the input of ball valve.
Dioxide bottle of the present utility model is provided with safety valve.
As shown from the above technical solution, the utility model mainly is to utilize carbon dioxide refrigerating effect per unit swept volume height, characteristics that evaporating pressure is high, utilize the dioxide bottle pressure inside, the carbon dioxide liquid of separating is pressed into evaporimeter, carry out sweat cooling, according to the gas storage capability of dioxide bottle, the refrigeration of corresponding time is provided, be implemented in the refrigeration when driving without any extrinsic motive.
Description of drawings
Fig. 1 is a systematic schematic diagram of the present utility model.
The specific embodiment
Below in conjunction with accompanying drawing the utility model is described further:
The self-driven refrigeration system of carbon dioxide as shown in Figure 1, by dioxide bottle 10, needle-valve 20, first cooling heat exchanger 30, second cooling heat exchanger 40, first capillary 50, gas-liquid separator 60, evaporimeter 70, blower fan 80, second capillary 90, heat exchanger 100, valve is connected in sequence by pipeline, the output of dioxide bottle 10 links to each other with the first input end of first cooling heat exchanger 30, first output of first cooling heat exchanger 30 links to each other with the first input end of second cooling heat exchanger 40, first output of second cooling heat exchanger 40 links to each other with the input of first capillary 50, valve comprises check valve 140 and stop valve 150, the output of heat exchanger 100 links to each other with the input of check valve 140, and the output of check valve 140 links to each other with the input of stop valve 150.
As preferred version of the present utility model, first cooling heat exchanger 30 also is provided with second input and second output, second cooling heat exchanger 40 also is provided with second input and second output, the gas output end of gas-liquid separator 60 links to each other with second input of second cooling heat exchanger 40, second output of second cooling heat exchanger 40 links to each other with the input of blower fan 80, the output of evaporimeter 70 links to each other with second input of first cooling heat exchanger 30, and second output of first cooling heat exchanger 30 links to each other with the input of blower fan 80.Like this, can the gas of discharging from gas-liquid separator 60 and evaporimeter 70 be cooled off once more, merge together, it is after 80s to drive blower fan, enters to continue evaporation in the heat exchanger 100 or utilize temperature difference heat absorption again, and refrigeration is better.
The concrete course of work is as follows:
Fluid flows out from dioxide bottle 10, adjust flow through needle-valve 20, first cooling heat exchanger 30 and second cooling heat exchanger, 40 priorities of flowing through are successively carried out twice cooling, reduced the enthalpy of carbon dioxide gas-liquid mixture, then flow directly into first capillary 50 and carry out throttling, as preferred version of the present utility model, be preferably 35bar through the pressure after 50 throttlings of first capillary; Fluid after the throttling enters gas-liquid separator 60, the liquid inflow evaporator of separating 70 evaporates heat absorption, reduce environment temperature, as preferred version of the present utility model, between the liquid output of separator 60 and evaporimeter 70, be provided with liquid-sighting glass 110, Pressure gauge 120 and thermometer 130 at gas, it is in order to observe the phasic property of refrigerant fluid, not had liquid if observe in the refrigerant flow path, showing that the refrigerating capacity of system is approaching exhausted that liquid-sighting glass 110 is set; Setting pressure table 120 and thermometer 130 are in order to determine the pressure and the temperature of internal flow, better control system; Refrigerant gas behind the outflow evaporimeter 70, second input of first cooling heat exchanger 30 of flowing through cools off, and second output by first cooling heat exchanger 30 flows out again; Second input that the gas that the gas output end of while gas-liquid separator 60 is separated enters second cooling heat exchanger 40 cools off, second output by second cooling heat exchanger 40 flows out again, converge mutually with the gas that flows out and cool off by evaporimeter 70 through first cooling heat exchanger 30, and can be used as the driving force of blower fan 80, blower fan 80 is sent into chilled air in the required environment and is gone.As preferred version of the present utility model, blower fan 80 is pneumatic blower fan, and in actual use, blower fan 80 also can change battery into and drive, and perhaps the two combination drive all is feasible; Gas after converging is through the second capillary 90 throttling step-down once more, as preferred version of the present utility model, pressure after the throttling this time is preferably 5.5bar, gas after the throttling heat exchanger 100 of flowing through again, in heat exchanger 100, part does not have the liquid of vapour warp to continue the evaporation heat absorption, cryogenic gas also carries out the heat exchange heat absorption by sensible heat and air at room temperature, the low-voltage high-temperature carbon dioxide gas basis of outflow heat exchanger 100, the check valve 140 of flowing through is again through stop valve 150, safe discharge system, because exhaust outlet also has certain pressure and carbon dioxide self characteristics, thus need enter in the atmospheric environment with certain flowability, and exhaust outlet upwards is provided with.
The beneficial effects of the utility model are embodied in: 1) need not extraneous any power, only need by the manual adjustments valve switch, realize continuing refrigeration, can be used as the standby refrigeration plant that needs to guarantee to continue refrigeration, guarantee the operate as normal of cooling system when power scatters and disappears; 2) cold-producing medium derives from atmosphere, enters atmosphere, the economic environmental protection of refrigeration mode; 3) the refrigeration system principle is simple, cooling operation reliability, safe; 4) manufacturing process maturation, each vitals of system equipment all can assemble by existing matured product, and production cost is low, is easy to promote.
Above-described embodiment is described preferred implementation of the present utility model; be not that scope of the present utility model is limited; under the prerequisite that does not break away from the utility model design spirit; various distortion and improvement that those of ordinary skills make the technical solution of the utility model all should fall in the definite protection domain of the utility model claims.
Claims (8)
1. self-driven refrigeration system of carbon dioxide, it is characterized in that: by dioxide bottle (10), needle-valve (20), first cooling heat exchanger (30), second cooling heat exchanger (40), first capillary (50), gas-liquid separator (60), evaporimeter (70), blower fan (80), second capillary (90), heat exchanger (100), valve is connected in sequence by pipeline, the output of dioxide bottle (10) links to each other with the first input end of first cooling heat exchanger (30), first output of first cooling heat exchanger (30) links to each other with the first input end of second cooling heat exchanger (40), and first output of second cooling heat exchanger (40) links to each other with the input of first capillary (50).
2. the self-driven refrigeration system of carbon dioxide according to claim 1, it is characterized in that: described first cooling heat exchanger (30) also is provided with second input and second output, and described second cooling heat exchanger (40) also is provided with second input and second output.
3. the self-driven refrigeration system of carbon dioxide according to claim 2, it is characterized in that: the gas output end of described gas-liquid separator (60) links to each other with second input of second cooling heat exchanger (40), and second output of second cooling heat exchanger (40) links to each other with the input of blower fan (80).
4. the self-driven refrigeration system of carbon dioxide according to claim 2, it is characterized in that: the output of evaporimeter (70) links to each other with second input of first cooling heat exchanger (30), and second output of first cooling heat exchanger (30) links to each other with the input of blower fan (80).
5. the self-driven refrigeration system of carbon dioxide according to claim 1 is characterized in that: be provided with liquid-sighting glass (110), Pressure gauge (120) and thermometer (130) between the liquid output of described gas-liquid separator (60) and the evaporimeter (70) successively.
6. according to any self-driven refrigeration system of the described carbon dioxide of claim among the claim 1-5, it is characterized in that: described blower fan (80) is pneumatic blower fan.
7. the self-driven refrigeration system of carbon dioxide according to claim 1, it is characterized in that: described valve comprises check valve (140) and stop valve (150), the output of heat exchanger (100) links to each other with the input of check valve (140), and the output of check valve (140) links to each other with the input of stop valve (150).
8. the self-driven refrigeration system of carbon dioxide according to claim 1 is characterized in that: described dioxide bottle is provided with safety valve (160).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200513076U CN201964680U (en) | 2011-03-01 | 2011-03-01 | Carbon dioxide self-driving refrigeration system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200513076U CN201964680U (en) | 2011-03-01 | 2011-03-01 | Carbon dioxide self-driving refrigeration system |
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| Publication Number | Publication Date |
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| CN201964680U true CN201964680U (en) | 2011-09-07 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN2011200513076U Expired - Fee Related CN201964680U (en) | 2011-03-01 | 2011-03-01 | Carbon dioxide self-driving refrigeration system |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102305490A (en) * | 2011-09-08 | 2012-01-04 | 南京航空航天大学 | Anti-icing-plug self-defrosting type carbon dioxide opened refrigerating system and method |
| CN104142033A (en) * | 2014-07-25 | 2014-11-12 | 北京市京科伦冷冻设备有限公司 | Carbon dioxide refrigeration device structure |
| CN105066504A (en) * | 2015-08-06 | 2015-11-18 | 浙江省江山市浙安消防设备有限公司 | Refrigeration device of cooling suit |
| CN110297530A (en) * | 2018-03-23 | 2019-10-01 | 宏碁股份有限公司 | Utilize the cooling means of liquefied gas |
-
2011
- 2011-03-01 CN CN2011200513076U patent/CN201964680U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102305490A (en) * | 2011-09-08 | 2012-01-04 | 南京航空航天大学 | Anti-icing-plug self-defrosting type carbon dioxide opened refrigerating system and method |
| CN104142033A (en) * | 2014-07-25 | 2014-11-12 | 北京市京科伦冷冻设备有限公司 | Carbon dioxide refrigeration device structure |
| CN105066504A (en) * | 2015-08-06 | 2015-11-18 | 浙江省江山市浙安消防设备有限公司 | Refrigeration device of cooling suit |
| CN110297530A (en) * | 2018-03-23 | 2019-10-01 | 宏碁股份有限公司 | Utilize the cooling means of liquefied gas |
| CN110297530B (en) * | 2018-03-23 | 2022-08-30 | 宏碁股份有限公司 | Cooling method using liquefied gas |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110907 Termination date: 20170301 |
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| CF01 | Termination of patent right due to non-payment of annual fee |